Nonwoven textiles or fabrics are suited to use in the filtration industry, due to the nature of randomly distributed fibers creating a torturous path for filtered contaminants to navigate, to stay in the fluid stream passing beyond the filter element. These engineered textiles are comprised of properties such as material type, fiber shape, fiber size, thickness, weight, density, etc., which can be varied to achieve specific goals suited to their application. Where some filter mediums favor high tensile strength for durability, others may comprise fine fibers for high filtration efficiency.
It is common for a composite filter medium to be made of different layers, combining the strengths of the individual layers into one product. For instance, when filtering fluid containing contaminants of a large range of sizes, a filter element may include a pre-filter that may be positioned on the upstream side of the remaining filter layers to capture and retain larger contaminants. Subsequent layers may be configured to filter smaller contaminants. These layers are sometimes referred to as depth layers, containing regions capable of capturing particulate, without drastically reducing flow, obstructing the path of the fluid stream. Depth filter layers can be made from various materials such as polypropylene, polyester, aramids, or cellulose constructed into needlefelts, spunbonds, or meltblown webs.
One high-filter-efficiency material is expanded polytetrafluoroethylene (ePTFE) membrane. For instance, ePTFE membrane may be commonly found as the primary filter layer in HEPA grade filter elements because it can achieve fine contaminant filtration with an acceptable pressure drop across the filter. Additionally, ePTFE membrane may provide hydrophobic qualities and a low coefficient of friction, allowing consumers to easily remove foreign bodies from the membrane surface without excessive washing procedures. However, ePTFE membrane may be delicate and poses challenges from handling to processing. For example, pleating of filter elements may commonly cause tearing of the membrane layer at the apex of the pleat tips if not produced carefully.
Alternative membrane mediums may be used to achieve high efficiency filtration status. One example would include but is not limited to ultra-high molecular weight polyethylene (UPE) membranes, such as ARIOSO by LYDALL Inc. of Manchester, Connecticut, USA.
Meltblown nonwoven filter mediums are another common type of primary filter medium that is capable of high efficiency filtration. These mediums are comprised of synthetic fibers, which are extruded and randomly distributed through a process of blowing gas at high velocities across the extrusion nozzles. This method of forming a filter medium lends itself to use of fine fiber sizes, capable of fine filtration. This fine filtration comes with the drawback of the meltblown layer being easily pulled apart, like tissue paper.
By placing a membrane or meltblown layer (herein referred to as the primary filter layer) between support layers or depth filter layers, the primary layer may be protected and may be more easily handled without damage. However, in conventional filter systems where a primary layer is bonded with other materials to form filter elements, the bonded regions may significantly restrict the fluid flow through the filter elements, resulting in lower filter system performance. Further, conventional methods of adhering multiple layers may be performed by a textile supplier as a unique operation step, possibly prior to being provided to an external textile converter to make into an end product. Isolating processing steps can add significant labor costs, as opposed to performing a sequence of operations in series, or inline.
When combining multiple layers of filter material, there is an inherent risk of the layers delaminating through excessive handling or otherwise. Sintering of fibers aids in increasing the bond between layers. Sintering occurs when the fibers are heated to a point that they soften, but do not reach a liquidation temperature.
Multiple-layer filter medium may be converted into filter elements, such as a die cut filter or a pleated filter. A die cut filter, may be a flat sheet of filter medium, or it can be intricately cut into a defined shape with or without empty cavities inside the perimeter bounds of the filter. A pleated filter element may have a series of undulations folded to maximize the filtration surface area within a given volume of the filter element.
Material rigidity allows the pleated filter element to maintain its desired shape, with roughly uniform āVā shaped pleats. During use for filtration, pressure may build on the upstream side of the filter medium. If the filter medium is not rigid enough, the pleats can bow. When substantial bowing occurs between two adjacent pleats, the surfaces of adjacent faces may touch or come so close together that the flow path of the filtered fluid is limited to a region along the pleat tips of one side of the filter. To combat this loss of filter area and maintain proper pleat shape and spacing, glue beads of hot melt adhesive, may be applied in line along the surface of the pleated filter element.
Some implementations herein include a bonded filter medium that may be usable as a filter element, or the like. For instance, the filter medium may include multiple layers of web (sheet) material, including a primary filter layer. The layers of web material may be bonded together in such a manner that the bonded areas do not obstruct the path of fluid flow.
Further, some examples herein are directed to techniques for concurrently cutting and sealing a primary filter layer sandwiched between outer layers of thermoplastic web material, such as through use of heated or ultrasonic slitting. The layers of thermoplastic web material may flow into one another at the slitting and bonding sites, creating a bond between the layers of thermoplastic web material along the perimeters of the thermoplastic web material and the primary filter layer, thereby encapsulating the primary filter layer between the layers of thermoplastic web material.
In some implementations, the bonding area is limited to the outermost regions of the filter medium's lateral extent, thereby allowing for the full extent of the medium's filtering area to be unencumbered by bonding agents. For instance, in conventional designs, regions bonded by densely packed thermoplastic or otherwise foreign adhesives cause an increase in pressure drop and may restrict fluid flow by as much as a factor of three. A filter element as described herein, without obstruction from bonding sites within the fluid path may include independent layers throughout the lateral extent of the filter, thereby decreasing pressure drop and providing optimal performance Thus, some examples include bonding multiple layers of material together to form a filter medium including a primary filter layer, which may be comprised of a membrane or a meltblown layer and without substantially reducing an area of the filter medium that is available for filtration. The multiple layers may be bonded along the edges of the filter medium concurrently with performing a process of slitting and/or trimming the width of the filter medium, and without obscuring the working filtration area of the filter medium between the bonded edges.
Producing a filter element, such as a pleated filter element, may include slitting a rolled sheet of multilayer filter medium to the appropriate size while concurrently bonding the edges of the filter medium as the filter medium enters the pleating equipment. Alternatively, in some cases, the filter medium may be rerolled and provided as a rolled good. Some examples herein may include positioning the slitting and bonding system in line with the pleating system to enable bonding of the multilayered filter medium composite to be performed concurrently with the slitting of the filter medium and subsequent pleating of the filter element. Thus, implementations herein may eliminate any need for point bonding or otherwise bonding the layers of the filter medium prior to the filter element production, thereby improving efficiency and achieving a cost savings through reduction in consumption of time and equipment resources.
Additionally, or alternatively, some examples may include positioning a membrane layer on an exterior upstream side of a composite filter medium, which may provide advantages in terms of washability of the filter medium. For instance, such a layer may be bonded along the lateral extents of the filter medium, as described previously, or may be heat laminated to the upstream side of a support layer comprised of a web of thermoplastic fibers. The low coefficient of friction and the hydrophobic nature of the membrane layer may allow for removal of foreign contaminants with relative ease, and without the need of replacing the filter.
With the layers 101, 102, 103 independent of each other, the filter medium 100 of
Each ultrasonic slitting assembly 210, 211 may include an ultrasonic horn 212, and a rotating anvil 213, 214, respectively. As the energy applied by the horn 212 is transferred through the respective material layers 101, 102, 103 against the cutting anvil 213, 214, the support material layers 101, 103 may flow into one another, creating an ultrasonic or thermal bond at the perimeter edges 110, 111. Due to the narrow shape of the anvils 213, 214, the material is separated laterally 220, 100, 221 on either side of the anvil along the perimeter edges 110, 111.
Continuing along the web path, the filter medium comprised of multiple layers 101, 102, 103 is now a bonded composite filter medium 100, including at least one primary filter layer 102 (e.g., ePTFE, meltblown nonwoven), at least one support layer 101 (e.g., thermoplastic web) upstream of the primary filter layer 102, and may also include at least one support layer 103 (e.g., thermoplastic web) downstream of the primary filter layer 102. Additional thermoplastic layers and/or primary filter layers can be added to form a multi-layered composite with as many total layers as desired for the specific end application. The multilayer composite filter medium 100 may be bonded solely along the lateral perimeter edges 110, 111 of a width of the filter medium 100, leaving the multiple layers free and unbonded 101, 102, 103 at all points between these lateral edges 110, 111. Lacking any bonded regions in the fluid path of the filter medium 100, allows for a decreased pressure drop, thus improving the efficiency of the filter system. The excess material at 220, 221 may be removed from the web path, and may be recycled or discarded.
Each laser slitting assembly 510, 511 is positioned to apply energy through the respective material layers 101, 102, 103 by means of a laser beam 512, 513, the support material layers 101, 103 may flow into one another, creating a thermal bond at the perimeter edges 110, 111. Similar to the process in
Each hot knife slitting assembly 610, 611 may include an anvil roller 612, and a heated knife element 613, 614, respectively. As the energy applied by the heated knives 613, 614 is transferred through the respective material layers 101, 102, 103 against the roller anvil 612, the support material layers 101, 103 may flow into one another, creating a thermal bond at the perimeter edges 110, 111.
Dependent on the material, some pleated filter elements 800, may have glue beads 811, 812 applied in lines along the length of the filter element 800. The conventional purpose of these glue beads 811, 812, is to maintain the shape and spacing between pleats, so that the filter performs its function maximizing the filter surface area and minimizing pressure drop across the filter element 800. These glue beads 811, 812 may have the added benefit in anchoring the individual layers of the filter element 800 together at desired intervals across the width of the filter. As the width of the filter medium increases, the flow pressure has an increasing force on the materials bonded. A buildup of foreign particulate may occur between individual layers, adversely constricting flow or increasing the pressure on discrete layers. Additional bond points, such as an increased number of glue beads 811, 812 may be employed to prevent delamination and optimize fluid flow.
This application claims the benefit of U.S. Provisional Patent Application No. 63/434,482, filed Dec. 22, 2022, and U.S. Provisional Patent Application No. 63/401,822, filed Aug. 29, 2022, both of which are incorporated by reference herein.
Number | Date | Country | |
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63434482 | Dec 2022 | US | |
63401822 | Aug 2022 | US |